ESP DESIGN AND OPERATION - LBCG...ESP DESIGN AND OPERATION April 29 – 30, 2015 CNQ ‒ An ESP is...

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PROVEN EFFECTIVE STRATEGY PREMIUM VALUE, DEFINED GROWTH, INDEPENDENT. ARTIFICIAL LIFT CONFERENCE ESP DESIGN AND OPERATION April 29 – 30, 2015

Transcript of ESP DESIGN AND OPERATION - LBCG...ESP DESIGN AND OPERATION April 29 – 30, 2015 CNQ ‒ An ESP is...

Page 1: ESP DESIGN AND OPERATION - LBCG...ESP DESIGN AND OPERATION April 29 – 30, 2015 CNQ ‒ An ESP is not just artificial lift tool it is an acceleration tool. ‒ Need to be able to

PROVEN EFFECTIVE STRATEGY

PREMIUM VALUE, DEFINED GROWTH, INDEPENDENT.

ARTIFICIAL LIFT CONFERENCE ESP DESIGN AND OPERATION

April 29 – 30, 2015

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CNQ

‒ An ESP is not just artificial lift tool it is an acceleration tool. ‒ Need to be able to justify the incremental cost with incremental

production. ‒ Does the increase in production result in incremental reserves or

accelerated production?

Is an ESP appropriate?

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Pro’s Cons

Can land around corners in deviated/horizontal wells

Large pump so sensitive to dog leg severity

High capacity Major equipment downhole

Can vary speeds with VFD Need to know the well

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• Complex system which needs to be in balance ‒ IPR/PI – need to know reservoir information as accurately as possible ‒ Pump – uses the IPR/PI information in its design ‒ Motor – matched to both the pump and the reservoir fluid ‒ Cable – matched to the motor and the required load ‒ Isolating transformer – filters dirty power, helps extend run life ‒ VFD – conditions the power to allow the motor to run at different speeds ‒ Tubing – friction losses a function of length, size and roughness ‒ Surface facilities - all sources of pressure loss increase tubing head

pressure

Production System

Slide 3

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Production Profile

•  Production characteristics are important ‒ How lively is your oil? ‒ How high is the water cut? ‒  Is GOR going up?

Slide 4

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Well vs Pump

•  Need accurate production data

Slide 5

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• Pump design requires the most complete and accurate input information possible.

• The better the inputs, the better the design.

Typical Pump Design Data Requirements

Slide 6

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Typical Pump Curve

Slide 7

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Material Selection

•  Corrosion potential from H2S and CO2 can shorten life - H2S leads to hydrogen embrittlement - CO2 corrosive with water

•  Abrasives have a dramatic effect. •  Work with the supplier to choose the best materials. •  Consider stocking long lead time special material parts.

Slide 8

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Motor Selection

•  Depending where you are in the range a size up might be better. •  Bigger motor will run cooler. •  Might also future proof for changes in fluid gradient or rate.

Slide 9

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Power, the Mysterious Variable

•  Electric switchgear can be a major weakness.

•  Poor power quality is probably a major cause of premature failure.

•  Modern VFD’s have more built in power conditioning than vintage equipment.

•  Other loads on the power grid can affect your power quality.

•  Match your equipment.

Slide 10

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Cable Selection

•  Cable might seem like an accessory but is a major component visa vis cost.

•  Cable sizing important, power losses can be significant.

•  Cable failure at connections/splices or where it comes through the wellhead are common.

•  Round cable is better than flat due to current underbalances characteristic of flat cable.

Slide 11

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Running the Pump

•  You are about to lower $200,000 of equipment down the well •  Check rig, both equipment and personnel.

Slide 12

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Running Cable

•  Cable spooler controls speed and therefore tension.

•  Need a skilled hand to coordinate with rig.

Slide 13

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Rig Equipment

•  Make sure the running equipment is appropriate

•  Brief the crew on nuisances of running a pump with cable.

Slide 14

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Amp Chart

Slide 15

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Sensors

•  Sensor is not just to hold down the motor. •  If you are going to run it, use it. •  Ideally tied in to monitoring system.

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Listen to the Pump

•  Startup data from the pump. You have to be there to get it. •  This pump failed in less than 2 hours from startup. •  Everything seemed to be going well until motor temperature starts to rise. •  Pump failed on overcurrent, ie, got too hot. •  Note temp difference between operating and failure was 25oF, probably wouldn’t

have noticed it on surface.

Slide 17

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Generic Measurements

•  Validate sensor information to increase confidence.

•  Tubing temperature and pressure to confirm flow

•  Casing pressure and fluid level confirm pump submergence.

•  Compare bottom hole pressure calculated from fluid level/casing pressure to that from sensor. You might not like what you see.

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24/7 Monitoring

•  If you have enough pumps and dedication, around the clock monitoring and decision making can increase run time.

Slide 19

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Failure Analysis

•  Tear down the pump and see what failed. Remember, a bad O-ring brought down the Challenger.

•  Documentation of the results will eventually result in a meaningful database

•  Industry cooperation has built large databases but analysis is still tricky.

•  Part of the benefit is tracking of surplus inventory.

•  CNRL belongs to a group that collects data which can be reported in different ways.

•  Minimum data set 38 data points, recommended data set 128 data points.

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Random Points

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• Storing cable for more than a year is not a good idea. The insulation deteriorates due to absorbed gas devolving.

• Suppliers often reserve the right to substitute materials. It takes a sharp eye to avoid becoming part of their R&D.

•  Individual parts are relatively cheap, don’t avoid replacing a questionable component to “save money”.

•  If you spend the money on a downhole sensor, collect and use the data. If you can’t measure it you can’t manage it.

• Seek out a corporate expert. A lot of major producers have people on staff who have an incredible knowledge base and whose interests are aligned with yours, they are not trying to sell you anything.

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PROVEN EFFECTIVE STRATEGY

PREMIUM VALUE, DEFINED GROWTH, INDEPENDENT.

THE PREMIUM VALUE, DEFINED GROWTH, INDEPENDENT.